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Catalyst precursor for hydrocracking reaction and method for hydrocracking heavy oil by using same

a catalyst and hydrocracking technology, applied in the direction of organic compound/hydride/coordination complex catalyst, physical/chemical process catalyst, metal/metal-oxide/metal-hydroxide catalyst, etc., to achieve the effect of increasing the economic value of the product by heavy oil cracking, easy supply and demand starting materials, and relatively cheap unit cos

Active Publication Date: 2022-11-08
KOREA RES INST OF CHEM TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0036]The catalyst precursor according to the present invention reacts with sulfur in a heavy oil to produce a molybdenum disulfide catalyst doped with phosphorus (P), and cracking of a low-grade heavy oil may be effectively derived by the catalyst. Specifically, a yield of a low-boiling point liquid product having a high economical value among the products by heavy oil cracking may be increased, and a yield of a relatively uneconomical gaseous product or coke (toluene-insoluble component) as a by-product may be significantly decreased.
[0037]In addition, the catalyst precursor according to the present invention may be derived from molybdenum oxide (MoO3) of which the unit cost is relatively cheap, and using the catalyst precursor makes it easy to supply and demand starting materials and has an economical advantage.
[0038]Thus, when a hydrocracking reaction through the catalyst precursor according to the present invention is applied, a high value-added liquid product (for example, a low-boiling point liquid product such as gasoline, kerosene, diesel, and naphtha) of which the boiling point corresponds to 30 to 524° C. may be provided with high selectivity from a low-grade residual oil discharged downstream of refinery, petrochemical, and steel industries or a high-boiling point heavy oil such as oil sand, pitch, and coal tar.BEST MODE
[0039]Hereinafter, the catalyst precursor for a hydrocracking reaction according to the present invention will be described in detail. Here, technical terms and scientific terms used in the present specification have the general meaning understood by those skilled in the art to which the present invention pertains unless otherwise defined, and a description for the known function and configuration which may unnecessarily obscure the gist of the present invention will be omitted in the following description.
[0040]The term of the present specification, “conversion (%)” refers to a ratio of a total amount of a liquid product and a gaseous product based on a weight of an entire product. The entire product refers to a total weight of a gaseous product, a liquid product, a residue, and coke.
[0041]In addition, the term of the present specification, “a liquid yield” refers to a ratio of a total amount of a liquid product (for example, naphtha, middle distillate, and gas oil) based on the weight of the entire product, during a hydrocracking reaction of a heavy oil.

Problems solved by technology

However, these carbon black, naphthalene, pitch, and the like have a relatively low added value and the range of use is limited.
In addition, due to a trend that crude oil becomes heavy and an increase in an impurity content in crude oil worldwide, a production proportion of a residual oil produced from a petroleum refinery is also increased, which causes a large increase in the burden of a post-treatment process such as conventional desulfurization equipment.
Among them, the heterogeneous iron oxide-based catalyst may be economically supplied, but a reaction temperature and a reaction temperature which are adjusted by an excessive hydrogen supply may be optimized under relatively severe conditions, resulting in high facility investment and operating costs.
However, the conventionally known catalyst as such has a problem of producing about 3 wt % of coke as an impurity, which is a relatively large amount.

Method used

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  • Catalyst precursor for hydrocracking reaction and method for hydrocracking heavy oil by using same
  • Catalyst precursor for hydrocracking reaction and method for hydrocracking heavy oil by using same
  • Catalyst precursor for hydrocracking reaction and method for hydrocracking heavy oil by using same

Examples

Experimental program
Comparison scheme
Effect test

example 2

[0118]Hydrocracking reaction using Mo(O)(O2)2(P(OEt)3)2

[0119]Step 1. A catalyst precursor for a hydrocracking reaction (Mo(O)(O2)2(P(OEt)3)2) was prepared under the same reaction conditions as Step 1 of Example 1, by using triethylphosphite instead of triphenylphosphine, as a ligand having a coordination number of 1 in Step 1 of Example 1.

[0120]1H-NMR (DMSO-d6, ppm): 1.23 (m, 18H), 3.98 (m, 12H)

[0121]13C-NMR (DMSO-d6, ppm): 15.90, 15.96, 63.01, 63.07

[0122]FT-IR (cm−1): 942, 983, 911, 803

[0123]Step 2. A hydrocracking reaction was performed under the same reaction condition as Step 2 of Example 1, by using the catalyst precursor for a hydrocracking reaction (Mo(O)(O2)2(P(OEt)3)2).

[0124]In addition, each product was analyzed according to the evaluation method of each step performed in Example 1, and the analysis results of the product produced after the hydrocracking reaction are shown in the following Table 3.

example 3

[0125]Hydrocracking Reaction Using Mo(O)(O2)2(PCy3)2

[0126]Step 1. A catalyst precursor for a hydrocracking reaction (Mo(O)(O2)2(PCy3)2) was prepared under the same reaction conditions as Step 1 of Example 1, by using tricyclohexanephosphine instead of triphenylphosphine, as a ligand having a coordination number of 1 in Step 1 of Example 1.

[0127]1H-NMR (CD2Cl2, ppm): 1.99 (m, 9H), 1.81 (d, 6H), 1.68 (s, 3H), 1.51 (t, 6H), 1.26 (s, 9H)

[0128]13C-NMR (CD2Cl2, ppm): 217.19 (Mo—CO), 37.72 (P—C—), 30.43 (—CH2—)

[0129]Step 2. A hydrocracking reaction was performed under the same reaction condition as Step 2 of Example 1, by using the catalyst precursor for a hydrocracking reaction (Mo(O)(O2)2(PCy3)2).

[0130]In addition, each product was analyzed according to the evaluation method of each step performed in Example 1, and the analysis results of the product produced after the hydrocracking reaction are shown in the following Table 3.

example 4

[0131]Hydrocracking Reaction Using Mo(C0)4(TOP)2

[0132]Step 1. To a 100 mL Schlenk tube substituted with argon, 1 g (3.8 mmol) of Mo(CO)6 and trioctylphosphine were dissolved in 10 ml of diethylene glycol dimethyl ether, and the reaction was performed at 150° C. for 20 hours. After the reaction, a supernatant was removed, and precipitates were washed once with distilled water and three times each with ethanol and ethyl ether and dried, thereby preparing a catalyst precursor for a hydrocracking reaction (Mo(CO)4(TOP)2).

[0133]1H-NMR (CDCl3, ppm): 1.64 (m 6H), 1.40 (m, 36H), 0.88 (t, 9H)

[0134]13C-NMR (CDCl3, ppm): 212.79 (M-CO), 31.93, 31.29, 29.37, 27.69, 26.10, 23.94, 22.78 (—CH2—), 14.21 (—CH2CH3)

[0135]FT-IR: 2922.4, 2853.3 (Octyl), 1877.4 cm−1 (Mo—CO)

[0136]Step 2. A hydrocracking reaction was performed under the same reaction condition as Step 2 of Example 1, by using the catalyst precursor for a hydrocracking reaction (Mo(CO)4(TOP)2).

[0137]In addition, each product was analyzed ac...

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Abstract

The present invention relates to a catalyst precursor for forming a molybdenum disulfide catalyst through a reaction with sulfur in heavy oil and to a method for hydrocracking heavy oil by using same. According to the present invention, the yield of a low-boiling liquid product with a high economic value in the products by heavy oil cracking can be increased, and the yield of a relatively uneconomical gas product or coke (toluene insoluble component), which is a byproduct, can be significantly lowered.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS[0001]This application is a national phase under 35 U.S.C. § 371 of PCT International Application No. PCT / KR2019 / 007776 which has an International filing date of Jun. 27, 2019, which claims priority to Korean Patent Application No. 10-2018-0082925, filed Jul. 17, 2018, the entire contents of each of which are hereby incorporated by reference.TECHNICAL FIELD[0002]The present invention relates to a catalyst precursor which reacts with sulfur in a heavy oil to form a molybdenum disulfide catalyst and a hydrocracking method of a heavy oil using the same.BACKGROUND ART[0003]In general, coke is prepared by carbonizing coking coal used in the steel industry. Here, a high-boiling point organic matter having a high carbon ratio is obtained, which is called coal tar, and in order to recycle produced coal tar, usually carbon black, naphthalene, pitch, and the like are produced by a pyrolysis process at a high temperature of 1200 K or higher. The thus-prod...

Claims

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Application Information

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Patent Type & Authority Patents(United States)
IPC IPC(8): C10G47/06B01J27/051B01J37/04B01J37/20C01G39/06C07F11/00
CPCC10G47/06B01J27/051B01J37/04B01J37/20C01G39/06C07F11/00C10G2300/202C10G2300/205C10G2300/4006C10G2300/4012C10G2300/70B01J23/28B01J27/19B01J31/2404B01J31/20B01J2531/64B01J31/185C07F11/005C10G2300/1048
Inventor PARK, SUNYOUNGLEE, CHUL WEEKIM, GYOO TAESEO, HWI MINCHUNG, MINEHULSON, SEOK HWANCHOI, BYONG MIN
Owner KOREA RES INST OF CHEM TECH